TW517107B - Improved clay-nylon polymer spinning properties - Google Patents
Improved clay-nylon polymer spinning properties Download PDFInfo
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Description
517107 五、發明說明(1) 本發明目的在於改善黏土尼龍聚合物之紡絲性及紡絲 所得纖維之物性。其所用的方法是使用分散劑處理黏土後 ,再和尼龍單體己内醯胺或己二胺和己二酸及水混合,經 過聚合反應得黏土尼龍聚合物,可以改善黏土尼龍聚合物 之紡絲性及機械性質,尤其當黏土含量大於2重量百分比 時,尤為明顯。 從美國專利文獻中可以發現用分散劑來處理黏土,然 後在和己内醯胺聚合反應得聚合物後,用來改善其在工程 塑膠或複合材料之用途時之耐熱性,如美國專利第5,747, 560號、美國專利第1^1^37,385£號、美國專利第5,102,9 48號、美國專利第5, 248, 720號、美國專利第5, 486, 573號 、美國專利第6, 121,361號、美國專利第6, 117, 931號、美 國專利第6, 103, 817號、美國專利第5, 973, 053號、美國專 利第5, 656, 7 09號等說明書便是。 本發明主要目的是使用5至18個碳之胺基酸為分散劑 ,其處理方式為將分散劑及黏土溶於水中,進行黏土分散 作用後,經過過濾烘乾後得粉末黏土。接著將分散劑處理 過之黏土與己内醯胺或己二胺和己二酸及水混合後,進行 聚合反應合成黏土尼龍聚合物,再紡成纖維,此時可得較 佳紡絲性及機械性質之纖維。 本發明在進行黏土分散過程中,要加入強酸(如鹽酸 、硫酸或麟酸專)於黏土、分散劑及水之混合液中,在室 溫至8 0 °C間進行攪拌均勻後過濾烘乾,便可得用分散劑處 理過之黏土粉末,其中水的用量為1至1 0 0倍於黏土重量,517107 V. Description of the invention (1) The purpose of the present invention is to improve the spinnability of clay nylon polymer and the physical properties of the fibers obtained by spinning. The method used is to treat the clay with a dispersant, and then mix it with the nylon monomers caprolactam or hexamethylenediamine and adipic acid and water, and polymerize to obtain a clay nylon polymer, which can improve the spinning of the clay nylon polymer. And mechanical properties, especially when the clay content is greater than 2 weight percent. It can be found from the U.S. patent literature that a clay is treated with a dispersant and then polymerized with caprolactam to obtain a polymer, which is used to improve its heat resistance in the application of engineering plastics or composite materials, such as U.S. Patent No. 5, 747, 560, U.S. Patent No. 1 ^ 1 ^ 37,385, U.S. Patent No. 5,102,9 48, U.S. Patent No. 5,248,720, U.S. Patent No. 5,486,573, U.S. Patent No. No. 6, 121,361, U.S. Patent No. 6,117,931, U.S. Patent No. 6,103,817, U.S. Patent No. 5,973,053, U.S. Patent No. 5,656,7 09, etc. Yes. The main purpose of the present invention is to use an amino acid having 5 to 18 carbons as a dispersant. The treatment method is to dissolve the dispersant and clay in water, disperse the clay, and filter and dry to obtain powdery clay. Then, the clay treated with the dispersant is mixed with caprolactam or hexamethylenediamine and adipic acid and water, and then polymerized to synthesize clay nylon polymer and then spin into fibers. At this time, better spinnability and mechanical properties can be obtained. Fiber of nature. In the process of clay dispersion of the present invention, a strong acid (such as hydrochloric acid, sulfuric acid, or linoleic acid) is added to a mixture of clay, dispersant, and water, and the mixture is stirred at room temperature to 80 ° C, and then filtered and dried. , You can get the clay powder treated with dispersant, in which the amount of water is 1 to 100 times the weight of the clay,
517107 五、發明說明(2) 主要目的是可攪拌均分既可。 本發明處理過之黏土的使用量為〇.〇1至1〇重量百分比 (以黏土尼龍聚合物為1 0 0重量百分比),而原來黏土需具 每1〇〇克黏土有50至2 〇〇毫當量之可交換陽離子(鈉或鈣離 子)’分散劑使用量為!升水使用i至1〇〇克,而強酸加入量 為0.05至5當量百分比,相對於未處理過黏土中全部可被 可交換陽離子(鈉或鈣離子)。 本發明所用的水要為去離子水或蒸餾水。 本發明再聚合過程所用尼龍單體可以為尼龍6單體己 内酿胺或尼龍66單體己二胺和己二酸或己二胺和己二酸之 鹽類。 本發明所提到黏土尼龍聚合反應過程中,可以加入一 些/肖光劑(如二氧化鈦),安定劑(如[rgan〇X lQl〇或磷酸) 及分子量控制劑(如醋酸或磷酸)等。 兹舉數個實施例說明如下,所舉實施例僅係對本發明 方法作概括性例示,並無限制本發明範圍之義,就此先作 聲明。 黏土分散處理: 20 0 克黏土(montmorillonite ;日本Yamagata517107 V. Description of the invention (2) The main purpose is to stir evenly. The used amount of the treated clay of the present invention is 0.01 to 10 weight percent (100 weight percent of clay nylon polymer), and the original clay needs to have 50 to 200 per 100 grams of clay. Milliquivalent exchangeable cations (sodium or calcium ions) 'dispersant is used in an amount! I to 100 g of water is used, and the strong acid is added in an amount of 0.05 to 5 equivalent percentages relative to all the exchangeable cations (sodium or calcium ions) in the untreated clay. The water used in the present invention is deionized water or distilled water. The nylon monomer used in the repolymerization process of the present invention may be a salt of nylon 6 monomer caprolactam or nylon 66 monomer hexamethylenediamine and adipic acid or adipic acid and adipic acid. In the polymerization process of the clay nylon mentioned in the present invention, some / xiaoguang agents (such as titanium dioxide), stabilizers (such as [rgan〇X lQl0 or phosphoric acid), and molecular weight control agents (such as acetic acid or phosphoric acid) can be added. A few examples are described below. The examples are merely general illustrations of the method of the present invention, and do not limit the scope of the present invention, and make a statement in this regard. Clay dispersion treatment: 200 grams of clay (montmorillonite; Yamagata, Japan
Prefecture公司產品,其可交換陽離子數為I〗g毫當量每 100克黏土)放入反應槽中,加入6升去離子水,再加入 102.4克12 -胺基月桂酸和48.2克濃磷酸,於室溫下攪拌6〇 分鐘後,過濾後,於1 〇 〇 °C烘乾可得黏土粉末。Products of Prefecture, whose exchangeable cation number is I (g milliequivalents per 100 grams of clay) are placed in a reaction tank, 6 liters of deionized water is added, and 102.4 grams of 12-aminolauric acid and 48.2 grams of concentrated phosphoric acid are added. After stirring at room temperature for 60 minutes, after filtering, drying at 100 ° C can obtain clay powder.
517107 五、發明說明(3) 實施例1 . 將上述處理過之黏土(用量見表1)和己内醯胺1〇〇公斤 及6克去離子水(相對於合成黏土尼龍聚物重量)放入2〇〇升 反應槽内,加熱攪拌均勻,在内溫升至26〇 t:過程中,若 壓力大於5kg/c rri時,便把壓力排至〇kg/c m2,等反應至2 小時後,便排壓至Okg/c rri,接著用氮氣吹約丨〇分鐘後, 便開始下料製粒,得黏土尼龍6聚合物粒子。 將上述黏土尼龍6聚合物粒子,在水裡水煮至重量不 再減輕後烘乾,然後用濃硫酸(96%)溶解後(濃度為1克 /1 00ml濃硫酸),使用黏度管Cannon-1於30 °C測其相對黏 度(結果見表1 )。 將上述水煮過之黏土尼龍6聚合物粒子烘乾後,經押 出機押出紡絲’其紡絲條件為聚合物溶融溫度為2 7 〇它, 押出機背壓為110kg/c m2,冷風溫度為室溫,冷風風速為 0.8m/sec,捲取速度為4 000至5〇〇〇m/min ,其絲每走右9 股,紡絲後物性見表卜 釆有24 比較例1. 步驟同實施例,只是所用黏土沒有用丨2—胺基月桂酸 和磷酸處理過,其結果見表1。 05 比較例1 表1 ·黏土尼龍6聚合物之紡絲後絲物性 編 號 01 0 2 〇3 〇4 樣品來源實施例1實施例1實施例1比較例j517107 V. Description of the invention (3) Example 1. Put the treated clay (see Table 1 for dosage) and 100 kg of caprolactam and 6 g of deionized water (relative to the weight of synthetic clay nylon polymer). In a 200-liter reaction tank, heat and stir uniformly, and the internal temperature rises to 260t: During the process, if the pressure is greater than 5kg / c rri, the pressure is discharged to 0kg / c m2, and the reaction is performed after 2 hours After depressurizing to Okg / crri, and then blowing with nitrogen for about 10 minutes, it began to cut and granulate to obtain clay nylon 6 polymer particles. The clay nylon 6 polymer particles are boiled in water until the weight is no longer reduced, and then dried, and then dissolved in concentrated sulfuric acid (96%) (concentration of 1 g / 1 00 ml of concentrated sulfuric acid), using a viscosity tube Cannon- 1 Measure its relative viscosity at 30 ° C (see Table 1 for results). After the above-mentioned boiled clay nylon 6 polymer particles are dried, they are spun out through an extruder. The spinning conditions are as follows: the polymer melting temperature is 27 ° C, the back pressure of the extruder is 110kg / c m2, and the temperature is cold. At room temperature, the cold wind speed is 0.8m / sec, and the take-up speed is 4,000 to 5000m / min. Each strand of the wire goes right 9 strands. See Table 24 for the physical properties after spinning. Comparative Example 1. Step In the same example, the clay used was not treated with 2-aminolauric acid and phosphoric acid. The results are shown in Table 1. 05 Comparative Example 1 Table 1 Silk Properties of Clay Nylon 6 Polymer after Spinning No. 01 0 2 〇3 〇4 Sample Source Example 1 Example 1 Example 1 Comparative Example j
第7頁 517107 五、發明說明(4) 黏土含量 0 2%(a) 5 %(a) 5%(b) 2°/〇(b) 相對黏度 2. 5 2. 7 3. 1 3. 2 2. 8 纖 度 70d/24f 70d/24f 70d/24f 70d/24f 70d/24f 纖維強度 4. Og/d 4· 2g/d 4.5g/d __ c L 8g/d (斷裂點) 纖細伸度 38% 3 6°/〇 34% — 37% 纖維模數 1 4g/d 20g/d 28g/d — 1 3g/d 係 數 成絲性 佳 佳 佳 斷絲很厲害 可 斷絲率 2 2 3 很多 3 (次/台·小時) 註··(1)黏土含量項中有a記號者表示其用之黏土有處理 過,b記號者表示黏土沒有處理過。 (2 )成絲性佳表示很好,可表示可接受。 從上表可以看出黏土有經分散劑處理過,其合成黏土 尼龍聚合物之成絲性佳,並且其纖維物性也較佳(尤其是 纖維模數係數更佳)。 實施例2. 將上述處理過黏土(其用量見表2)和己二胺及己二酸 (己二胺和己二酸之莫耳比;共1〇〇公斤)及6克去離 子水放入20 0升反應槽内,加熱攪拌均勻後,升溫至28〇Page 7 517107 V. Description of the invention (4) Clay content 0 2% (a) 5% (a) 5% (b) 2 ° / 〇 (b) Relative viscosity 2.5 5 2. 7 3. 1 3.2 2. 8 fineness 70d / 24f 70d / 24f 70d / 24f 70d / 24f 70d / 24f fiber strength 4. Og / d 4 · 2g / d 4.5g / d __ c L 8g / d (break point) slim elongation 38% 3 6 ° / 〇34% — 37% Fiber modulus 1 4g / d 20g / d 28g / d — 1 3g / d Coefficient of silk formation good Allison wire breakage is very good Broken wire rate 2 2 3 Many 3 (times / Set · hour) Note ... (1) Those with a mark in the clay content item indicate that the clay they used has been treated, and those with a b mark indicate that the clay has not been treated. (2) Good silk formation indicates good, and can indicate acceptable. It can be seen from the table above that the clay has been treated with a dispersant, and its synthetic clay nylon polymer has good silk-forming properties, and its fiber properties are also better (especially the fiber modulus is better). Example 2. The treated clay (the dosage is shown in Table 2), hexamethylene diamine and adipic acid (molar ratio of hexamethylene diamine and adipic acid; 100 kg in total) and 6 g of deionized water were placed in 20 In a 0 liter reaction tank, heat up and stir to 28 ° C.
第8頁 517107 發明說明 C2 f升溫過程中當壓力大於5kg/c m2時,便排壓至〇kg/c =二^到反應時間至3小時後,便排壓至〇kg/c m2,然後用 氮氣吹約1 0分鐘,便開始下料製粒,得黏土尼龍6 6聚合物 粒子。然後取黏土尼龍6 6粒子烘乾後,溶於96%濃硫酸裡 (濃度為1克/100毫升),黏度管使用編號為Unnon—丨測其 相對黏度。 將上述合成黏土尼龍6 6聚合物粒子烘乾後,經由押出 機押出紡絲,其紡絲條件為聚合物熔融溫度為2 9 〇艽,押 出機背壓為120kg/cm2,冷風速度為室溫〇.9m/ sec.,捲取 速度為4000至50 00m/min·,其紡絲後物性見表2.。 比較例2. 步驟同實施例2,只是所用黏土沒有用1 2-胺基月桂酸 和磷酸處理過。 表2.黏土尼龍66聚合物之紡絲後物性 編 號 11 12 13 樣 品 來 源 實施例2 實施例2 比較例2 黏 土 含 量 0 5°/〇(a) 5 %(b) 相 對 黏 度 2. 7 3. 4 3. 5 纖 度 70d/24f 70d/24f 70d/24f 纖 維 強 度 4·lg/d 4· 7g/d — (斷裂點) 纖 維 伸 度 36% 36% —Page 8 517107 Description of the invention During C2 f heating, when the pressure is greater than 5 kg / c m2, the pressure will be reduced to 0 kg / c = 2 ^ After the reaction time to 3 hours, the pressure will be reduced to 0 kg / c m2, and then Nitrogen was blown for about 10 minutes, and then feeding and granulation were started to obtain clay nylon 66 polymer particles. Then the clay nylon 6 6 particles were dried and dissolved in 96% concentrated sulfuric acid (concentration: 1 g / 100 ml). The viscosity of the tube was measured using the number Unnon—. After drying the synthetic clay nylon 6 6 polymer particles, the spinning conditions are as follows: the polymer melt temperature is 290 ° F, the back pressure of the extruder is 120 kg / cm2, and the cold air speed is room temperature. 0.9 m / sec., The take-up speed is 4000 to 50,000 m / min ·, and its physical properties after spinning are shown in Table 2. Comparative Example 2. The procedure was the same as in Example 2, except that the clay used was not treated with 1 2-aminolauric acid and phosphoric acid. Table 2. Physical properties of clay nylon 66 polymer after spinning No. 11 12 13 Sample source Example 2 Example 2 Comparative Example 2 Clay content 0 5 ° / 〇 (a) 5% (b) Relative viscosity 2.73. 4 3. 5 Fineness 70d / 24f 70d / 24f 70d / 24f Fiber strength 4 · lg / d 4 · 7g / d — (break point) Fiber elongation 36% 36% —
517107 五、發明說明(6) 纖維模數係數 15g/d 29g/d — 成 絲 性 佳 佳 斷絲很厲害 斷 絲 率 2 3 很多 (次/台· 小時) 註:(1)黏土含量項中有a記號者表示其用之黏土有 . 處理過,b記號者表示黏土沒有處理過。 (2 )成絲性佳表示很好,可表示可接受。 ^517107 V. Description of the invention (6) Fiber modulus 15g / d 29g / d — good filament formation, good broken wire, very strong broken rate 2 3 many (times / set · hour) Note: (1) clay content Those with a mark indicate that the clay they have used has been treated, and those with b mark indicate that the clay has not been treated. (2) Good silk formation indicates good, and can indicate acceptable. ^
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